Method and apparatus for continuous sulfonization of discrete article

ABSTRACT

An apparatus for continuous sulfonization of discrete articles using ultra-dry air, sulfur trioxide gas, and a neutralizing fluid includes a sulfonization chamber for treating the discrete articles with sulfur trioxide gas, the sulfonization chamber including a chamber bottom having a circular periphery extending about a center axis and defining a chamber bottom opening on the center axis, the chamber wall having a cylindrical shape extending upwardly about the circular periphery of the chamber bottom and perpendicular to the chamber bottom, and a rotating dial plate having a circular periphery and presenting an upper surface extending radially from and rotatable about the center axis and disposed above the chamber bottom for receiving the discrete articles at the circular periphery of the rotating dial plate.

CROSS-REFERENCE TO RELATED APPLICATION(S)

The present application is a divisional application of U.S. Ser. No. 13/167,330, filed Jun. 23, 2011, the entire content of which is hereby incorporated by reference.

BACKGROUND OF THE INVENTION

1. Field of the Invention

An apparatus for continuous sulfonization of discrete articles using ultra-dry air, sulfur trioxide gas, and a neutralizing fluid.

2. Description of the Prior Art

The sulfonization apparatuses of the type to which the subject invention pertains continuously treat the surfaces of discrete articles with ultra-dry air, sulfur trioxide gas, and neutralizing fluid. One such apparatus is illustrated in U.S. Pat. No. 6,719,848 to Faykosh et al. wherein the apparatus treats glass sheet substrates with a chemical vapor as they move along a straight conveyor. This apparatus has a chamber bottom with a circular periphery extending about a center axis and defines a chamber bottom opening on the center axis. Another such apparatus is illustrated in U.S. Pat. No. 6,758,910 to Schmoyer wherein dry air and sulfur trioxide gas are mixed to treat discrete articles in a sulfonization apparatus. This apparatus also includes a chamber bottom with a circular periphery extending about a center axis and defines a chamber bottom opening on the center axis for loading and unloading the discrete articles onto a rack inside the sulfonization apparatus for batch treatment of the articles. In addition, the Schmoyer patent shows the feature of employing a neutralizing fluid to the discrete articles after the ultra-dry air and sulfur trioxide gas treatments are employed.

These prior-art sulfonization apparatuses use either straight line conveyors or treatment of discrete articles in separate batches. The straight line conveyor may need to be very long or move at a very slow speed to allow sufficient treatment time for the articles on the conveyor. Using a batch treatment process requires loading and unloading of discrete articles into an apparatus of restricted size and also requires a fixed period of time to treat each batch of discrete articles. Neither method allows an efficient use of both time and space in continuous treatment of discrete articles with sulfur trioxide gas.

SUMMARY OF THE INVENTION

The subject invention provides such a sulfonization apparatus wherein the sulfonization chamber includes a rotating dial plate with a circular periphery and an upper surface extending radially from and rotatable about a center axis for receiving the discrete articles at the circular periphery of the rotating dial plate.

The invention also provides a method for continuous sulfonization of discrete articles characterized by the steps of transferring the discrete articles one at a time in a continuous stream from the feeder box to the outer periphery of the sulfonization chamber, rotating the discrete articles a pre-determined number of revolutions per minute about a center axis (A) of the sulfonization chamber, moving the rotating discrete articles radially inward from the outer periphery of the sulfonization chamber in a spiral path toward the center axis of the sulfonization chamber, treating the discrete articles with the sulfur trioxide gas as the discrete articles move in the spiral path, and transporting the discrete articles at the center axis through a chamber bottom opening at the center axis to the neutralizing tank.

ADVANTAGES OF THE INVENTION

The subject invention provides for both time and space efficient continuous treatment of discrete articles with ultra-dry air, sulfur trioxide gas, and neutralizing fluid. Using a rotating dial plate for movement of the discrete articles within the sulfonization chamber combines several advantages in the prior art while eliminating disadvantages. Using a rotating dial which moves the discrete articles inwardly toward a central axis along a spiral path allows for continuous treatment of the discrete articles without the need for a long conveyor or a short conveyor moving at slow, inefficient speeds. Use of the rotating dial plate to move the discrete articles also allows the sulfonization apparatus to use less space than would be needed by a straight conveyor. Additionally, the rotating dial plate allows the use of a small space similar to a batch-process apparatus while avoiding the delays in loading and unloading batches and the restriction of processing only one batch at a time.

BRIEF DESCRIPTION OF THE DRAWINGS

Other advantages of the present invention will be readily appreciated, as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings wherein:

FIG. 1 is a front elevation view showing the sulfonization apparatus of the subject invention;

FIG. 2 is a front elevation view showing the sulfonization apparatus of the subject invention with each top removed;

FIG. 3 is a cross-sectional view of FIG. 1 through section B-B;

FIG. 4 is a top view of FIG. 2.

DETAILED DESCRIPTION OF THE ENABLING EMBODIMENTS

Referring to the Figures, wherein like numerals indicate corresponding parts throughout the several views, an apparatus for continuous sulfonization of discrete articles using ultra-dry air, sulfur trioxide gas, and a neutralizing fluid constructed in accordance with the subject invention is shown in FIGS. 1, 2, 3, and 4.

The sulfonization apparatus includes a feeder box 20, generally indicated, for drying the discrete articles with ultra-dry air. The feeder box is constructed from a box bottom 22 having a rectangular periphery and a plurality of box sides 24 extending upwardly 10 about the rectangular periphery and perpendicular to the box bottom 22 to define an open top. The feeder box includes a box liner 26 extending parallel to the box bottom 22 and upwardly along a portion of the box sides 24 for providing a cushion to the discrete articles within the feeder box 20. The feeder box also includes a box top 28 perpendicular to the box sides 24 and parallel to the box bottom 22 for closing the open top defined by the box sides 24. The box top 28 includes a pair of handles 30 for facilitating manual removal of the box top 28 from the feeder box allowing an operator to load the discrete articles into the feeder box 20.

A first of the box sides 24 defines a plurality of access openings 32 for allowing access to the discrete articles. A plurality of covers 34 having a glove-like shape are disposed on the first box side 24 and about the access openings 32 for allowing manual access to the discrete articles within the feeder box 20. An operator can use the glove-like covers 34 to manipulate the discrete articles in the feeder box without negatively impacting the drying process. A second of the box sides 24 defines an exit opening 36 for allowing transfer of the discrete articles from the feeder box after they complete the drying process. The second box side 24 extends perpendicularly from the first box side 24 in the preferred embodiment.

One of the box sides 24 of the feeder box also defines an air inlet opening 38 for introducing the ultra-dry air into the feeder box 20. The box bottom 22 defines a plurality of box perforations 40 for circulating the ultra-dry air through the box bottom 22 and out of the feeder box 20. The ultra-dry air enters the feeder box through the air inlet opening 38 and exits the box through the box perforations 40 in the box bottom 22.

The sulfonization apparatus also includes a sulfonization chamber 42, generally indicated, for treating the discrete articles with sulfur trioxide gas. The sulfonization chamber 42 includes a chamber bottom 44 having a circular periphery extending about a center axis A and defines a chamber bottom opening 46 on the center axis A for transferring the discrete articles out of the sulfonization chamber 42. In the preferred embodiment, the sulfonization chamber 42 is constructed of stainless steel, inconel, fluoropolymer-based material, or any other material resistant to extreme acidity.

The sulfonization chamber 42 includes a dial mount 48 disposed upon the chamber bottom 44 and extending about and radially spaced from the chamber bottom opening 46. The sulfonization chamber 42 also includes a rotating dial plate 50 having a circular periphery rotatably supported on the dial mount 48 about the center axis A and extending parallel to and spaced from the chamber bottom 44. The rotating dial plate 50 presents an upper surface 52 extending radially from the center axis A and disposed above the chamber bottom 44 for receiving the discrete articles at the circular periphery of the rotating dial plate 50. In the preferred embodiment, the rotating dial plate 50 is also constructed of stainless steel, inconel, fluoropolymer-based material, or any other material resistant to extreme acidity.

The sulfonization chamber 42 also includes a chamber wall 54 and a chamber top 56 supported on the chamber wall 54. The chamber wall 54 has a cylindrical shape extending upwardly about the circular periphery of the chamber bottom 44 and perpendicular to the chamber bottom 44. The chamber wall 54 defines an entrance opening 58 for allowing transfer of the discrete articles into the sulfonization chamber 42 and onto the upper surface 52 of the rotating dial plate 50. The chamber wall 54 also defines a gas inlet opening 60 for allowing sulfur trioxide gas into the sulfonization chamber 42 to treat the discrete articles. The chamber top 56 is frustoconical in shape about the center axis A and defines an exhaust opening 62 on the center axis A for exhausting the sulfur trioxide gas.

The chamber wall 54 includes a guide arm 64 extending parallel to and spaced from the upper surface 52 of the rotating dial plate 50. The guide arm 64 includes a plurality of guides 66 being arcuate in shape and extending perpendicularly from the guide arm 64 toward the upper surface 52 of the rotating dial plate 50 and spaced radially outward from one another along a radial R extending radially from the center axis A for moving the discrete articles radially inward in a spiral path during rotation of the rotating dial plate 50. In the preferred embodiment, the rotating dial plate 50 will travel between one half and one revolution per minute to slowly move the discrete articles along the spiral path while they are treated with the sulfur trioxide gas.

A first of the guides 66 includes a first end 68 for receiving the discrete articles and extends in a spiral about the center axis A to a second end 70 for positioning the discrete articles radially inward for alignment with the first end 68 of a next of the guides 66 spaced radially inward from the first of the guides 66 for moving the discrete articles progressively and radially inward in response to successive rotations of the rotating dial plate 50.

In other words, the spacing and shape of the guides 66 allow the discrete articles to move successively inward in a spiral path through each of the guides 66 on the upper surface 52 of the rotating dial plate 50.

The sulfonization chamber 42 also includes a gas inlet tube 72 with a pair of tube legs 74 disposed on opposite sides of the gas inlet opening 60 and between the chamber bottom 44 and the rotating dial plate 50 and spaced apart from the center axis A for distributing the sulfur trioxide gas into the sulfonization chamber 42. The gas inlet tube 72 defines tube perforations 80 for distributed introduction of the sulfur trioxide gas into the sulfonization chamber 42 below the rotating dial plate 50. The rotating dial plate 50 also defines a plurality of dial perforations 82 for circulating the sulfur trioxide gas through the rotating dial plate 50 and into the sulfonization chamber 42. In other words, the preferred embodiment has the sulfur trioxide gas entering the sulfonization chamber 42 through the tube perforations 80 and traveling upwardly through the dial perforations 82 to treat the discrete articles on the rotating dial plate 50 before exiting the sulfonization chamber 42 through the exhaust opening 62.

The rotating dial plate 50 defines a dial opening 84 about the center axis A spaced axially from the chamber bottom opening 46 for transferring the discrete articles from the rotating dial plate 50 after the discrete articles reach the dial opening 84. The diameter and speed of the rotating dial plate 50 defines the length of time the discrete articles are treated in the sulfonization chamber 42 with the sulfur trioxide gas.

The sulfonization apparatus also includes a conveyor assembly 86, generally indicated, extending between the feeder box and the sulfonization chamber 42 for transporting the discrete articles from the feeder box to the sulfonization chamber 42. The conveyor assembly 86 includes a conveyor housing 88 comprised of a plurality of housing sides 76 defining an interior channel 90 extending between the exit opening 36 of the feeder box and tangentially to the entrance opening 58 of the sulfonization chamber 42.

The conveyor assembly 86 also includes a conveyor 92 extending from a third box side 24 opposite the second box side 24 and adjacent the first box side 24 through the exit opening 36 and the conveyor housing 88 to the entrance opening 58 of the sulfonization chamber 42 for transporting the discrete articles from the feeder box to the sulfonization chamber 42. Manual loading of the discrete articles onto the conveyer is completed inside the feeder box to avoid contamination of the discrete articles after they are dried with ultra-dry air.

The sulfonization apparatus also includes a neutralizing tank 94, generally indicated, for receiving the discrete articles from the sulfonization chamber 42 and for treating the discrete articles with neutralizing fluid. The neutralizing tank 94 includes a tank bottom 96 having a rectangular periphery and a plurality of tank sides 78 extending upwardly about the periphery and perpendicular to the tank bottom 96 for holding the neutralizing fluid. A tank top 98 is supported by the tank sides 78 perpendicular to the tank sides 78 and parallel to the tank bottom 96. The tank top 98 defines a tank opening 100 for receiving the discrete articles from the sulfonization chamber 42.

The sulfonization apparatus also includes an exit tube 102 extending between the sulfonization chamber 42 and the neutralizing tank 94 for transporting the discrete articles from the sulfonization chamber 42 to the neutralizing tank 94. The exit tube 102 has a cylindrical shape and extends from the dial opening 84 through the chamber bottom opening 46 and the tank opening 100 to the neutralizing tank 94 for guiding gravitational movement of the discrete articles from the rotating dial plate 50 and into the neutralizing tank 94 after the discrete articles complete the spiral path on the upper surface 52 of the rotating dial plate 50. The exit tube 102 includes a trap door 104 disposed within the exit tube 102 parallel to the tank bottom 96 for closing the exit tube 102 and containing the neutralizing fluid within the neutralizing tank 94.

As alluded to above, the subject invention also includes a method for continuous sulfonization of discrete articles including drying the discrete articles with ultra-dry air in a feeder box 20, treating the discrete articles with sulfur trioxide gas in a sulfonization chamber 42, and treating the discrete articles with neutralizing fluid in a neutralizing tank 94.

The sulfonization process begins by loading the discrete articles into the feeder box and feeding the ultra-dry air into the feeder box to dry the discrete articles. Once dry, the discrete articles are transferred one at a time in a continuous stream from the feeder box to the outer periphery of the sulfonization chamber 42. The loading and transferring of discrete articles can be done manually by operators, automatically by machines, or using a combination of manual and automatic steps.

In the sulfonization chamber 42, the discrete articles are rotated a pre-determined number of revolutions per minute about a center axis A of the sulfonization chamber 42. In the preferred embodiment, the discrete articles move between one-half and one revolution per minute. The rotation of the discrete articles is further defined by placing the discrete articles on a rotating dial plate 50 having a circular periphery and presenting an upper surface 52 and disposed in the sulfonization chamber 42 for carrying the discrete articles.

While the discrete articles rotate about the center axis A on the rotating dial plate 50, they are moved radially inward from the outer periphery of the sulfonization chamber 42 in a spiral path toward the center axis A of the sulfonization chamber 42. The movement of the rotating discrete articles radially inward is further defined by using a plurality of arcuate guides 66 extending perpendicularly from the upper surface 52 and spaced radially outward from one another along a radial R extending radially from the center axis A of the sulfonization chamber 42. In other words, each of the plurality of guides 66 moves the discrete articles radially inward toward the center axis A on the upper surface 52 of the rotating dial plate 50.

During movement along the spiral path, the discrete articles are treated with the sulfur trioxide gas. Once the discrete articles reach the center axis A, the discrete articles are transported through a chamber bottom opening 46 at the center axis A to a neutralizing tank 94. The discrete articles are treated with the neutralizing fluid in the neutralizing tank 94. After the neutralizing treatment, the discrete articles are removed from the neutralizing tank 94 to complete the sulfonization process.

Obviously, many modifications and variations of the present invention are possible in light of the above teachings and may be practiced otherwise than as specifically described while within the scope of the appended claims. That which is prior art in the claims precedes the novelty set forth in the “characterized by” clause. The novelty is meant to be particularly and distinctly recited in the “characterized by” clause whereas the antecedent recitations merely set forth the old and well-known combination in which the invention resides. These antecedent recitations should be interpreted to cover any combination in which the inventive novelty exercises its utility. The use of the word “said” in the apparatus claims refers to an antecedent that is a positive recitation meant to be included in the coverage of the claims whereas the word “the” precedes a word not meant to be included in the coverage of the claims. In addition, the reference numerals in the claims are merely for convenience and are not to be read in any way as limiting. 

What is claimed is:
 1. An apparatus for continuous sulfonization of discrete articles using ultra-dry air, sulfur trioxide gas, and a neutralizing fluid comprising: a sulfonization chamber for treating the discrete articles with sulfur trioxide gas; said sulfonization chamber including a chamber bottom having a circular periphery extending about a center axis and defining a chamber bottom opening on said center axis; said chamber wall having a cylindrical shape extending upwardly about the circular periphery of the chamber bottom and perpendicular to said chamber bottom; and a rotating dial plate having a circular periphery and presenting an upper surface extending radially from and rotatable about said center axis and disposed above said chamber bottom for receiving the discrete articles at said circular periphery of said rotating dial plate.
 2. A sulfonization apparatus as set forth in claim 1 wherein said chamber wall includes a guide arm extending parallel to and spaced from the upper surface of the rotating dial plate, and said guide arm includes a plurality of guides being arcuate in shape extending perpendicularly from the guide arm toward said upper surface of the rotating dial plate and spaced radially outward from one another along a radial extending radially from said center axis for moving the discrete articles radially inward in a spiral path during rotation of said rotating dial plate.
 3. A sulfonization apparatus as set forth in claim 2 wherein a first of said guides includes a first end for receiving the discrete articles extending in a spiral about said center axis to a second end for positioning the discrete articles radially inward for alignment with said first end of a next of said guides spaced radially inward from said first of said guides for moving the discrete articles progressively and radially inward in response to successive rotations of said rotating dial plate.
 4. A sulfonization apparatus as set forth in claim 1 wherein said rotating dial plate defines a plurality of dial perforations for circulating the sulfur trioxide gas through said rotating dial plate and into said sulfonization chamber.
 5. A sulfonization apparatus as set forth in claim 1 wherein said rotating dial plate defines a dial opening about said center axis.
 6. A sulfonization apparatus as set forth in claim 1 wherein said sulfonization chamber includes a dial mount disposed on said chamber bottom and extending about and radially spaced from said chamber bottom opening.
 7. A sulfonization apparatus as set forth in claim 6 wherein said rotating dial plate is rotatably supported by said dial mount and extends parallel to and spaced from said chamber bottom.
 8. A sulfonization apparatus as set forth in claim 1 wherein said chamber wall defines an entrance opening for allowing transfer of the discrete articles into said sulfonization chamber and a gas inlet opening for allowing sulfur trioxide gas into said sulfonization chamber.
 9. A sulfonization apparatus as set forth in claim 8 wherein said sulfonization chamber includes a gas inlet tube including a pair of tube legs disposed on opposite sides of said gas inlet opening and between said chamber bottom and said rotating dial plate and spaced apart from said center axis.
 10. A sulfonization apparatus as set forth in claim 9 wherein said gas inlet tube defines tube perforations for introducing the sulfur trioxide gas into said sulfonization chamber.
 11. A sulfonization apparatus as set forth in claim 1 wherein said sulfonization chamber includes a chamber top being supported on said chamber wall.
 12. A sulfonization apparatus as set forth in claim 11 wherein said chamber top being frustoconical in shape about said center axis defines an exhaust opening on said center axis for exhausting the sulfur trioxide gas.
 13. A sulfonization apparatus as set forth in claim 1 further comprising a feeder box for drying the discrete articles with ultra-dry air.
 14. A sulfonization apparatus as set forth in claim 13 wherein said feeder box includes a box bottom having a rectangular periphery and a plurality of box sides extending upwardly about said rectangular periphery and perpendicular to said box bottom to define an open top.
 15. A sulfonization apparatus as set forth in claim 14 wherein said feeder box includes a box liner extending parallel to said box bottom and upwardly along said box sides between said box bottom and said conveyor assembly for providing a cushion to the discrete articles within said feeder box.
 16. A sulfonization apparatus as set forth in claim 14 wherein one of said box sides of said feeder box defines an air inlet opening for introducing the ultra-dry air into said feeder box.
 17. A sulfonization apparatus as set forth in claim 14 wherein said box bottom of said feeder box defines a plurality of box perforations for circulating the ultra-dry air through said box bottom and out of said feeder box.
 18. A sulfonization apparatus as set forth in claim 14 wherein a first of said box sides defines a plurality of access openings for allowing access to the discrete articles within said feeder box.
 19. A sulfonization apparatus as set forth in claim 18 wherein said feeder box includes a plurality of covers having a glove-like shape disposed on said first box side and about said access openings for allowing manual access to the discrete articles within said feeder box.
 20. A sulfonization apparatus as set forth in claim 18 wherein a second of said box sides defines an exit opening for allowing transfer of the discrete articles from said feeder box.
 21. A sulfonization apparatus as set forth in claim 20 wherein said second box side of said feeder box extends perpendicularly from said first box side.
 22. A sulfonization apparatus as set forth in claim 14 wherein said feeder box includes a box top perpendicular to said box sides and parallel to said box bottom for closing said open top defined by said box sides.
 23. A sulfonization apparatus as set forth in claim 22 wherein said box top includes a pair of handles for facilitating manual removal of said box top from said feeder box.
 24. A sulfonization apparatus as set forth in claim 13 further comprising a conveyor assembly extending between said feeder box and said sulfonization chamber for transporting the discrete articles from said feeder box to said sulfonization chamber.
 25. A sulfonization apparatus as set forth in claim 24 wherein said conveyor assembly includes a conveyor housing including a plurality of housing sides defining an interior channel extending between said exit opening of said feeder box and tangentially to said entrance opening of said sulfonization chamber.
 26. A sulfonization apparatus as set forth in claim 25 wherein said conveyor assembly includes a conveyor extending from a third box side opposite said second box side and adjacent said first box side of said feeder box through said exit opening and said conveyor housing to said entrance opening of said sulfonization chamber for transporting the discrete articles from said feeder box to said sulfonization chamber.
 27. A sulfonization apparatus as set forth in claim 1 further comprising a neutralizing tank for receiving the discrete articles from said sulfonization chamber and for treating the discrete articles with neutralizing fluid.
 28. A sulfonization apparatus as set forth in claim 27 wherein said neutralizing tank includes a tank bottom having a rectangular periphery and a plurality of tank sides extending upwardly about said periphery and perpendicular to said tank bottom for holding the neutralizing fluid.
 29. A sulfonization apparatus as set forth in claim 28 wherein said neutralizing tank includes a tank top perpendicular to said tank sides and parallel to said tank bottom supported on said tank sides.
 30. A sulfonization apparatus as set forth in claim 29 wherein said tank top defines a tank opening for receiving the discrete articles from said sulfonization chamber.
 31. A sulfonization apparatus as set forth in claim 27 further comprising an exit tube extending between said sulfonization chamber and said neutralizing tank for transporting the discrete articles from said sulfonization chamber to said neutralizing tank.
 32. A sulfonization apparatus as set forth in claim 31 wherein said exit tube having a cylindrical shape extends from said dial opening through said chamber bottom opening and said tank opening to said neutralizing tank for guiding gravitational movement of the discrete articles from said rotating dial plate and into said neutralizing tank.
 33. A sulfonization apparatus as set forth in claim 31 wherein said exit tube includes a trap door disposed within said exit tube parallel to said tank bottom for closing said exit tube and containing the neutralizing fluid within said neutralizing tank.
 34. An apparatus for continuous sulfonization of discrete articles using ultra-dry air, sulfur trioxide gas, and a neutralizing fluid comprising: a feeder box for drying the discrete articles with ultra-dry air; a sulfonization chamber for treating the discrete articles with sulfur trioxide gas; a conveyor assembly extending between said feeder box and said sulfonization chamber for transporting the discrete articles from said feeder box to said sulfonization chamber; a neutralizing tank for receiving the discrete articles from said sulfonization chamber and for treating the discrete articles with neutralizing fluid; an exit tube extending between said sulfonization chamber and said neutralizing tank for transporting the discrete articles from said sulfonization chamber to said neutralizing tank; said feeder box including a box bottom having a rectangular periphery and a plurality of box sides extending upwardly about said rectangular periphery and perpendicular to said box bottom to define an open top; said feeder box including a box liner extending parallel to said box bottom and upwardly along said box sides between said box bottom and said conveyor assembly for providing a cushion to the discrete articles within said feeder box; said feeder box including a box top perpendicular to said box sides and parallel to said box bottom for closing said open top defined by said box sides; said box top including a pair of handles for facilitating manual removal of said box top from said feeder box; a first of said box sides defining a plurality of access openings for allowing access to the discrete articles within said feeder box; a second of said box sides defining an exit opening for allowing transfer of the discrete articles from said feeder box; one of said box sides of said feeder box defining an air inlet opening for introducing the ultra-dry air into said feeder box; said sulfonization chamber including a chamber bottom having a circular periphery extending about a center axis and defining a chamber bottom opening on said center axis; said sulfonization chamber including a chamber wall having a cylindrical shape extending upwardly about said circular periphery of said chamber bottom and perpendicular to said chamber bottom; said sulfonization chamber including a chamber top supported on said chamber wall, said chamber wall defining an entrance opening for allowing transfer of the discrete articles into said sulfonization chamber, said chamber wall defining a gas inlet opening; said conveyor assembly including a conveyor housing including a plurality of housing sides defining an interior channel extending between said exit opening of said feeder box and tangentially to said entrance opening of said sulfonization chamber; said neutralizing tank including a tank bottom having a rectangular periphery and a plurality of tank sides extending upwardly about said periphery and perpendicular to said tank bottom for holding the neutralizing fluid; said neutralizing tank including a tank top perpendicular to said tank sides and parallel to said tank bottom supported on said tank sides; a rotating dial plate having a circular periphery and presenting an upper surface extending radially from and rotatable about said center axis and disposed above said chamber bottom for receiving the discrete articles at said circular periphery of said rotating dial plate; said chamber wall including a guide arm extending parallel to and spaced from the upper surface of the rotating dial plate, said guide arm including a plurality of guides being arcuate in shape and extending perpendicularly from said guide arm toward said upper surface of said rotating dial plate and spaced radially outward from one another along a radial extending radially from said center axis for moving the discrete articles radially inward in a spiral path during rotation of said rotating dial plate; a first of said guides including a first end for receiving the discrete articles and extending in a spiral about said center axis to a second end for positioning the discrete articles radially inward for alignment with said first end of a next of said guides spaced radially inward from said first of said guides for moving the discrete articles progressively and radially inward in response to successive rotations of said rotating dial plate; said rotating dial plate defining a plurality of dial perforations for circulating the sulfur trioxide gas through said rotating dial plate and into said sulfonization chamber; said sulfonization chamber including a dial mount disposed upon said chamber bottom and extending about and radially spaced from said chamber bottom opening; said rotating dial plate being rotatably supported by said dial mount and extending parallel to and spaced from said chamber bottom, said rotating dial plate defining a dial opening about said center axis; said box bottom of said feeder box defining a plurality of box perforations for circulating the ultra-dry air through said box bottom and out of said feeder box; said second box side of said feeder box extending perpendicularly from said first box side; said feeder box including a plurality of covers having a glove-like shape disposed on said first box side and about said access openings for allowing manual access to the discrete articles within said feeder box; said chamber top of said sulfonization chamber being frustoconical in shape about said center axis and defining an exhaust opening on said center axis for exhausting the sulfur trioxide gas; said sulfonization chamber including a gas inlet tube including a pair of tube legs disposed on opposite sides of said gas inlet opening and between said chamber bottom and said rotating dial plate and spaced apart from said center axis; said gas inlet tube defining tube perforations for introducing the sulfur trioxide gas into said sulfonization chamber; said conveyor assembly including a conveyor extending from a third box side opposite said second box side and adjacent said first box side through said exit opening and said conveyor housing to said entrance opening of said sulfonization chamber for transporting the discrete articles from said feeder box to said sulfonization chamber; said tank top defining a tank opening for receiving the discrete articles from said sulfonization chamber; said exit tube having a cylindrical shape and extending from said dial opening through said chamber bottom opening and said tank opening to said neutralizing tank for guiding gravitational movement of the discrete articles from said rotating dial plate and into said neutralizing tank; and said exit tube including a trap door disposed within said exit tube parallel to said tank bottom for closing said exit tube and containing the neutralizing fluid within said neutralizing tank. 